Crosslinked organic-inorganic hybrid membranes and their use in gas separation

ABSTRACT

The present invention is for crosslinked membranes and in particular for crosslinked poly(ethylene oxide)-cellulose acetate-silsesquioxane (PEO-CA-Si) organic-inorganic hybrid membranes and their use in gas separation. These crosslinked PEO-CA-Si membranes were prepared by in-situ sol-gel co-condensation of crosslinkable PEO-organotrialkoxysilane and CA-organotrialkoxysilane polymers in the presence of acetic acid catalyst during the formation of membranes. The crosslinkable PEO- and CA-organotrialkoxysilane polymers were synthesized via the reaction between the hydroxyl groups on PEO (or on CA) and the isocyanate on organotrialkoxysilane to form urethane linkages under mild conditions. The crosslinked PEO-CA-Si membranes exhibited both increased selectivity of CO 2 /N 2  and CO 2  permeability as compared to a CA membrane, suggesting that these membranes are very promising for gas separations such as CO 2 /N 2  separation.

CROSS-REFERENCE TO RELATED APPLICATION

This application is a Continuation of application Ser. No. 12/131,392 filed Jun. 2, 2008, now U.S. Pat. No. 7,790,803, the contents of which are hereby incorporated by reference in its entirety.

BACKGROUND OF THE INVENTION

This invention pertains to crosslinked organic-inorganic hybrid membranes. More specifically, this invention pertains to crosslinked poly(ethylene oxide)-cellulose acetate-silsesquioxane (PEO-CA-Si) organic-inorganic hybrid membranes and methods of making these membranes. This invention also pertains to the application of these membranes for gas separations such as CO₂/N₂ separation.

CO₂ is an impurity that must be removed from mixtures with light gases such as CH₄, N₂ and H₂, and the scale of these separations is enormous. See Kohl, et al., GAS PURIFICATION, Fifth Ed., Gulf Publishing, Houston, Tex., 1997. Membrane-based separation of CO₂ from gas streams is an important unit operation. Separations of CO₂ with membranes include natural gas purification, CO₂ capture from flue gas (primarily in mixtures with N₂), and metabolic CO₂ removal from space life-supporting systems (extravehicular mobility unit (EMU), space shuttle or space station), and CO₂ removal from H₂.

General public awareness concerning the atmospheric greenhouse or “greenhouse warming” effect attributed to CO₂ has created the need to devise environmentally friendly and energy efficient technologies for the removal of CO₂ from industrial waste gas streams. Flue gas from fossil fuel power generation (primarily in mixtures with N₂) is the largest single contributor to CO₂ emissions. Therefore, CO₂ recovery from flue gas is becoming more important due to global warming. Generally, flue gas has a large volume and a relatively low concentration in CO₂ (typically 10-20 mol-%). Membrane-based separation of CO₂ from flue gas holds great promise due to its low energy consumption, low cost, easy operation, and low maintenance. A membrane system with a high processing capacity and a reasonably high selectivity for CO₂/N₂ is required in order to compete with other separation techniques such as physical or chemical absorption, low temperature distillation and pressure swing adsorption.

Separation of CO₂ from flue gas (mainly N₂) with commonly used polymeric membranes (e.g. cellulose acetate and fluorine-containing polyimides) or inorganic membranes (e.g. zeolite, sol-gel silica or carbon molecular sieve) is achieved by differences in diffusion rates and/or adsorption strengths of mixture components in the polymer matrix or the inorganic membrane pores, and selectivity is usually rather low, e.g. approximately 20 for CO₂/N₂ at about 50° C. for gas mixtures. See Baker, IND. ENG. CHEM. RES., 41: 1393 (2002); Tsai, et al., J. MEMBR. SCI., 169: 255 (2000). On the other hand, facilitated transports of CO₂ in ion-exchange or immobilized liquid membranes have been intensively investigated because they have high selectivity due to the chemical interaction between CO₂ and carrier molecules. See Baltus, et al., SEP. SCI. TECH., 40: 525 (2005). For example, a number of recently developed immobilized liquid membranes exhibited high (>1000) CO₂/N₂ selectivity due to facilitated CO₂ transport mechanism. However, there are still no practical applications for this type of membranes mainly because their CO₂ permeation rate is rather low especially at moderate levels of relative humidity (<40%), and also the durability and retention of the liquid in real process conditions are poor. See Kovvali, et al., IND. ENG. CHEM. RES., 40: 2502 (2001); Kovvali, et al., IND. ENG. CHEM. RES., 41: 2287 (2002).

Polymer blends have been the focus of extensive gas membrane separation research since 1980's. For example, poly(ethylene glycol) (PEG) and cellulose acetate or cellulose nitrate blend membranes have been investigated for CO₂/N₂ separation. It has been reported that PEG can dissolve substantial amounts of sour gases such as CO₂, and the diffusivity of large penetrants such as CO₂ and CH₄ in PEG may be high, considering its flexible main chain. A miscible blend membrane containing 10 wt-% of PEG with molecular weight of 20,000 showed both higher CO₂/N₂ selectivity and CO₂ permeability than those of the cellulose acetate membrane. See Li, et al., J. APPL. POLYM. SCI., 58: 1455 (1995). These blend polymers containing PEG, however, still have issues of durability and retention of the liquid PEG for real industrial applications.

To solve the longer term stability problem of PEG (or poly(ethylene oxide), PEO)-based polymer membranes, various techniques have been reported to crosslink PEG or PEO. For instance, radiation or radical crosslinking of PEG or PEO has been reported. Crosslinking by reactions of end groups such as hydroxyl or vinyl groups has been studied. See Lin et al., J. MOL. STR., 739: 57 (2005); Lin, et al., MACROMOLECULES, 38: 8394 (2005); Lin, et al., MACROMOLECULES, 38: 8381 (2005). All of these crosslinked PEG- or PEO-based membranes are organic polymeric membranes without the presence of inorganic segments, therefore, issues related to chemical resistance, thermal stability, and pressure stability (e.g. plasticization or swelling of membrane) may still exist. In addition, this type of crosslinked organic polymeric membranes has never been fabricated into asymmetric hollow fiber or flat sheet membranes possibly because they cannot be easily integrated into current polymer membrane manufacturing process using phase-inversion technique.

SUMMARY OF THE INVENTION

In order to overcome the inherent disadvantages of the existing membranes and to enhance gas separation performance, this invention provides for crosslinked organic-inorganic hybrid membranes with interchain-connected cellulose acetate and poly(ethylene oxide) organic polymers through covalently bound inorganic silsesquioxane ligands.

In general, the invention provides for crosslinked organic-inorganic hybrid membranes. More specifically, the present invention involves the preparation of crosslinked poly(ethylene oxide)-cellulose acetate-silsesquioxane (PEO-CA-Si) organic-inorganic hybrid membranes containing covalent bonds between the cellulose acetate (CA) and the poly(ethylene oxide) (PEO) polymer chains and their application for gas separations such as separation of carbon dioxide and nitrogen. These crosslinked PEO-CA-Si membranes with covalently interpolymer-chain-connected hybrid networks were prepared by simple in-situ sol-gel co-condensation of crosslinkable PEO-organotrialkoxysilane and CA-organotrialkoxysilane polymers in the presence of acetic acid catalyst during the formation of membranes. The crosslinkable PEO- and CA-organotrialkoxysilane polymers are synthesized via the reaction between the hydroxyl groups on PEO (or on CA) and the isocyanate on organotrialkoxysilane to form a urethane linkage under mild conditions.

These crosslinked organic-inorganic hybrid polymer membranes provide favorable characteristics including the following: First, the hard cellulose acetate and inorganic silsesquioxane segments provide good mechanical strength, the inorganic silsesquioxane crosslinking segments also offer good chemical resistance, high thermal and pressure stabilities, and the soft PEO segments offer high permeability because of the high mobility for polyether chains. Second, the strong affinity of the PEO segments for CO₂ molecules is believed to result in the high CO₂/N₂ selectivity. Third, the degree of crosslinking for the crosslinked organic-inorganic hybrid membranes can be easily controlled by adjusting the ratio of precursor organic CA and PEO polymers and the organosilicon alkoxide crosslinking agent. Fourth, these crosslinked organic-inorganic hybrid polymer membranes are different from organic-inorganic hybrid mixed matrix membranes in that there is no inorganic particle size issue, and they have much better chemical and mechanical stabilities compared to organic-inorganic hybrid mixed matrix membranes due to the existence of covalent bonds between the organic and inorganic segments; Fifth, the crosslinked PEO-CA-Si membranes in this invention can be easily integrated into current CA polymer membrane manufacturing process due to their simplified synthetic procedure compared to the crosslinked PEO dense film prepared by free radical polymerization method in the literature.

The crosslinked PEO-CA-Si membranes exhibited both significantly enhanced permeability of CO₂ (increased up to 60%) and greatly improved selectivity of CO₂/N₂ (increased up to 30%) compared to a cellulose acetate membrane. This improved selectivity means that these membranes are very promising for gas separations such as CO₂/N₂, olefin/paraffin, aromatics/non-aromatics, polar molecules such as H₂O, H₂S, SO₂ and NH₃/mixtures with CH₄, N₂, H₂, air, and other light gases separations.

DETAILED DESCRIPTION OF THE INVENTION

In recent years, numerous efforts have been focused on design of polymers containing poly(ethylene glycol) (PEG) or poly(ethylene oxide) (PEO) segments for CO₂/N₂ and CO₂/H₂ separations mainly because of the unique properties of the polar ether oxygen in PEG or PEO for CO₂ separations. However, the low molecular weight PEOs are in liquid phase and the solid-state high molecular weight PEOs are subject to a strong tendency to crystallize, which are deleterious conditions for gas permeability.

Crosslinking is a useful technique to convert liquid-state low molecular weight PEO to solid-state PEO and to reduce crystallinity in high molecular weight PEO. Crosslinking is also a useful method to improve the gas separation performance of polymer membranes. Crosslinking of polymers can provide crosslinked polymers with higher T_(g) than un-crosslinked polymers. Therefore, the crosslinked polymer membranes always have a high resistance to plasticization, and exhibit excellent thermal and chemical stability, enhanced selectivity of gas pairs, improved mechanical stability, or enhanced contaminant resistance than the uncrosslinked polymer membranes. The membrane crosslinking methods include thermal treatment, radiation, chemical crosslinking, UV-photochemical, blending with other polymers, etc. See Koros, et al., US 20030221559 (2003); Jorgensen, et al., US 2004261616 (2004); Patel, et al., ADV. FUNC. MATER., 14 (7): 699 (2004); Patel, et al., MACROMOL. CHEM. PHY., 205: 2409 (2004).

There has been only a little work that has focused on crosslinking of polymeric membranes using inorganic materials. This invention pertains to crosslinked organic-inorganic hybrid membranes. More specifically, this invention pertains to crosslinked poly(ethylene oxide)-cellulose acetate-silsesquioxane (PEO-CA-Si) organic-inorganic hybrid membranes and methods of making the same. This invention also pertains to the application of these crosslinked poly(ethylene oxide)-cellulose acetate-silsesquioxane (PEO-CA-Si) organic-inorganic hybrid membranes for gas separations such as the CO₂/N₂ separation.

The crosslinked PEO-CA-Si organic-inorganic hybrid membranes were prepared by in-situ sol-gel co-condensation of crosslinkable PEO-organotrialkoxysilane and CA-organotrialkoxysilane polymers in the presence of acetic acid catalyst during the formation of the membranes. The crosslinked PEO-CA-Si organic-inorganic hybrid membranes can also be prepared from crosslinkable polypropylene oxide-ethylene oxide-propylene oxide) (PPO-PEO-PPO tri-block co-polymer containing PEO segment)-organotrialkoxysilane and CA-organotrialkoxysilane polymers in the presence of acetic acid catalyst during the formation of the membranes. The crosslinkable PEO- and CA-organotrialkoxysilane polymers were synthesized via the reaction between the hydroxyl groups on PEO (the molecular weight of PEO can be varied, e.g. PEO400 and PEO1500 with molecular weights (M_(n)) of 400 and 1500, respectively) or CA and the isocyanate on the organotrialkoxysilane to form urethane linkages under mild conditions. All kinds of PEO polymers with different molecular weights in liquid or solid state can be used for the preparation of this new type of crosslinked organic-inorganic hybrid membranes. In addition, PPO-PEO-PPO tri-block co-polymer with different molecular weights (e.g. PPO-PEO-PPO2000 with M_(n)=2000) can also be used for the preparation of this new type of crosslinked organic-inorganic hybrid membranes. The crosslinkable PPO-PEO-PPO-organotrialkoxysilane polymers can be prepared via the reaction between the amino groups on both ends of PPO-PEO-PPO tri-block co-polymer and the epoxy group on the organotrialkoxysilane to form imine linkage under mild reaction conditions. Subsequent in-situ hydrolysis and condensation of these crosslinkable precursor polymers during the membrane-forming process yielded crosslinked organic-inorganic hybrid polymer membranes with covalently interpolymer-chain-connected hybrid networks.

The crosslinkable precursor polymers are prepared by reaction of the precursor polymer such as polyethylene oxide with an organosilicon alkoxide in the presence of a solvent such as tetrahydrofuran. The crosslinked organic-inorganic polymers are made by the sol-gel polymerization of two or more of these crosslinkable precursor polymers which may be solution cast as a dense film or otherwise used as a membrane.

Typical polymers as the precursor organic polymer suitable for the preparation of crosslinked organic-inorganic hybrid polymer membranes can be selected from any rubbery or glassy polymers containing organic functional groups on terminals or on the side chains of the polymer backbones (or called macromolecular backbones). The organic functional groups on the precursor organic polymer can be hydroxyl, amino, epoxy, isocyanato, dianhydride, etc. Example precursor organic polymers include poly(ethylene oxide)s (PEO), cellulose acetates (CA), poly(propylene oxide)s (PPO), co-block-poly(ethylene oxide)-poly(propylene oxide)s (PEO-PPO), tri-block-poly(propylene oxide)-poly(ethylene oxide)-poly(propylene oxide)s (PPO-PEO-PPO), poly(propylene glycol)-block-poly(ethylene glycol)-block-poly(propylene glycol) bis(2-aminopropyl ether) (PAPE), dendritic PEO, and hyperbranched amine-terminated PEO.

The organosilicon alkoxide crosslinking agents used to form covalent bonds with the precursor organic polymer should have two characteristics. One is that these organosilicon alkoxide crosslinking agents should contain at least one organic functional group that can react with the organic functional groups on the precursor organic polymer. The other is that these organosilicon alkoxide crosslinking agents should have at least two silicon alkoxide groups that can crosslinked with each other via a sol-gel condensation polymerization to form a fully crosslinked inter-polymer-chain network.

In the structure for the organosilicon alkoxide, n=−2−10; m=3; R′ is an organic functional group which may include of —(CH₂)_(a)NH₂ (a=1−20), —(CH₂)_(a)OH (a=1−20), —(CH₂)_(a)NH(CH₂)₂NH₂ (a=1−20), OCH₂CH(OH)CH₂N(CH₂CH₂OH)₂, —(CH₂)_(a)N═C═O (a=1−20), —(CH₂)_(a)CH(O)CH₂ (a=1−20), and mixtures thereof; R″ is a C1-C8 hydrocarbon group.

The crosslinking catalysts used to catalyze the sol-gel polymerization can be selected from either bases or acids. More preferably, the crosslinking catalysts are selected from weak acids such as acetic acid or hydrochloric acid.

The successful formation of urethane linkages between organic PEO and CA polymers and the inorganic silsesquioxane segments were confirmed by FTIR spectra. The crosslinked CA-silsesquioxane membrane showed the appearance of a vibration band at about 1568 cm⁻¹ corresponding to NH—CO group, indicating the formation of urethane linkages.

In this invention, crosslinked PEO-CA-Si organic-inorganic hybrid membranes were prepared that exhibited the advantages of the organic PEO polyether segments and CA polymer matrix, as well as the advanced features of inorganic silsesquioxane crosslinking segments. Ten to fifty percent by weight of the crosslinkable PEO-organotrialkoxysilane polymers were added to crosslinkable CA-organotrialkoxysilane polymers.

The permeability (P) and ideal selectivity (α_(CO2/N2)) of the crosslinked PEO-CA-Si organic-inorganic hybrid membranes were measured by pure gas measurements at 50° C. under approximately 690 kPa (100 psig) pressure. As shown in Table 1, the crosslinked PEO-CA-Si organic-inorganic hybrid membranes offer both enhanced P_(CO2) and α_(CO2/N2) compared to those of the pure CA polymer membrane, suggesting this new type of crosslinked PEO-CA-Si organic-inorganic hybrid membranes is very promising for gas separation applications of such as for CO₂ removal from flue gas (mainly N₂).

For example, as shown in Table 1, the P_(CO2) of crosslinked 30% PPO-PEO-PPO2000-CA-Si with 30 wt-% of PPO-PEO-PPO2000-Si segments (12.2 Barrer) increased approximately 60% over that of pure CA dense film (7.56 Barrer), and in the meantime the α_(CO2/N2) (29.8) increased approximately 25% compared to that of pure CA dense film (α_(CO2)N₂=23.7). For another example, the P_(CO2) of crosslinked 30% PEO400-CA-Si with 30 wt-% of PEO400—Si segments (10.6 Barrer) increased approximately 40% over that of pure CA dense film (7.56 Barrer), and in the meantime the α_(CO2/N2) (31.1) increased approximately 30% compared to that of pure CA dense film (α_(CO2/N2)=23.7).

Pure gas permeation results for the crosslinked PEO-CA-Si organic-inorganic hybrid membranes in this invention (Table 1) were compared with those of the CA-PEG uncrosslinked blend membranes reported in the literature (Table 2, see Li, et al., J. APPL. POLYM. S_(CI.,) 58: 1455 (1995)). It can been seen from Table 2 that the uncrosslinked blend CA-PEG membranes containing 10 wt-% of PEG200, PEG600, and PEG2000 with PEG molecular weights of 200, 600, and 2000, respectively, showed very poor CO₂/N₂ selectivity of less than 15 without improvement for CO₂ permeability compared to pure CA membrane. While as shown in Table 1, the crosslinked PEO-CA-Si membranes prepared by chemical crosslinking approach described in this invention containing 30 wt-% of PEO400, PEG1500, or PPO-PEO-PPO2000 with molecular weights of 400, 1500, and 2000, respectively, exhibited both greatly improved CO₂/N₂ selectivities and CO₂ permeability compared to the pure CA membrane. These results demonstrated the effectiveness of the chemical crosslinking approach to improve the CO₂/N₂ gas separation performance of CA-PEO blend membranes.

The crosslinked organic-inorganic hybrid polymer membranes described in this invention can be used for a variety of liquid and gas separations such as CO₂/N₂, olefin/paraffin, aromatics/non-aromatics, polar molecules such as H₂O, H₂₅, SO₂, and NH₃/mixtures with CH₄, N₂, H₂, air, and other light gas separations.

TABLE 1 Pure gas permeation test results of CA and crosslinked PEO-CA-Si membranes ^(a) Crosslinked 30% Crosslinked 30% Crosslinked 30% PPO-PEO-CA- Film Pure CA PEO400-CA-Si PEO1500-CA-Si PPO2000-Si P_(CO) ₂ (Barrer) 7.56 10.6 10.4 12.2 ΔP_(CO) ₂ (Barrer) 0 40.2% 37.6% 61.4% P_(N) ₂ (Barrer) 0.319 0.341 0.362 0.410 α_(CO) ₂ _(/N) ₂ 23.7 31.1 28.7 29.8 Δα_(CO) ₂ _(/N) ₂ 0 31.2% 21.1% 25.7% P_(CH) ₄ (Barrer) 0.321 0.525 0.548 0.649 α_(CO) ₂ _(/CH) ₄ 23.6 20.2 19.0 18.7 ^(a) Tested at 50° C. under 690 kPa (100 psig). 1 Barrer = 10⁻¹⁰ cm³(STP) · cm/cm² · sec · cmHg.

TABLE 2 Pure gas permeation test results of CA and its blend membranes containing PEG^(a) CA + 10% CA + 10% CA + 10% CA + 10% CA + 10% Film CA PEG200 PEG600 PEG2000 PEG6000 PEG20000 P_(CO) ₂ _((Barrer)) 5.96 4.92 5.72 6.30 6.16 7.49 P_(N) ₂ _((Barrer)) 0.231 0.918 0.418 0.452 0.194 0.207 P_(CH) ₄ _((Barrer)) 0.205 1.14 0.831 0.549 0.247 0.248 P_(O) ₂ _((Barrer)) 1.05 1.46 1.22 1.10 — 0.993 P_(H) ₂ _((Barrer)) 14.9 22.2 14.8 13.8 10.9 11.4 D_(CO) ₂ 0.560 0.475 0.639 0.723 0.929 1.00 (×10⁸ cm²/sec) S_(CO) ₂ 106 104 89.5 80.4 66.3 74.6 (×10³ cm³(STP)/cm³·cmHg) α_(CO) ₂ _(/N) ₂ 25.8 5.36 13.7 13.9 31.7 36.2 α_(CO) ₂ _(/CH) ₄ 29.2 4.31 6.88 11.5 25.0 30.3 ^(a)Tested at 35° C. under 27 kPa (3.9 psig); Table from literature Li, et al., J. APPL. POLYM. SCI., 58: 1455 (1995). 1 Barrer = 10⁻¹⁰ cm³(STP) · cm/cm² · sec · cmHg.

Example 1 Synthesis of Crosslinkable Cellulose Acetate (CA)-Organotriethoxysilane Hybrid Polymer

5.0 g (18.9 mmol) of CA polymer was dissolved in 100.0 g of THF or 1,4-dioxane solvent. 1.29 g (5.2 mmol) of 3-isocyanatopropyltriethoxysilane was added to the CA solution. After the solution was heated at 60° C. for 24 hours, the crosslinkable CA-organotriethoxysilane hybrid polymer solution was obtained.

Example 2 Synthesis of Crosslinkable PEO-Organotriethoxysilane Hybrid Polymers

The crosslinkable PEO-organotriethoxysilane hybrid polymers were synthesized from the reaction between PEO400 (M_(n)=400) or PEO1500 (M_(n)=1500) polymer and 3-isocyanatopropyltriethoxysilane with PEO400 (or PEO1500) to 3-isocyanatopropyltriethox-ysilane molar ratio of 1:2 using the same procedure as described in Example 1.

Example 3 Synthesis of Crosslinkable PPO-PEO-PPO-Organotriethoxysilane Hybrid Polymer

The crosslinkable PPO-PEO-PPO-organotriethoxysilane was synthesized from the reaction between poly(propylene glycol)-block-poly(ethylene glycol)-block-poly(propylene glycol) bis(2-aminopropyl ether) (PPO-PEO-PPO with M_(n)=2000) and (3-glycidoxypropyl) trimethoxysilane with PPO-PEO-PPO to (3-glycidoxypropyl)trimethoxysilane molar ratio of 1:2 according to the same procedure as that for the crosslinkable CA-organotriethoxysilane except that the reaction was conducted at room temperature.

Example 4 Preparation of Crosslinked PEO-CA-Si Organic-Inorganic Hybrid Polymer Membranes

A catalytic amount of acetic acid (0.01 g, 0.17 mmol) was added to 18.38 g of a polymer solution in 1,4-dioxane or THF containing 0.708 g (2.13 mmol) of crosslinkable CA-organotriethoxysilane prepared in Example 1 and 0.212 g of PEO400-organotriethoxysilane polymer (or PEO1500-organotriethoxysilane polymer) prepared in Example 2 followed by the addition of 0.01 g (0.22 mmol) of ethanol. The resulting solution was mixed for at least 6 hours at room temperature. The solution was then filtered through a 0.2 μm PTFE membrane filter. 16 g of the filtrate solution containing about 0.8 g of total polymers was cast onto the surface of a clean glass plate, and dried at room temperature for 24 hours. The resulting crosslinked PEO-CA-Si hybrid polymer membrane was detached from the glass plate and further dried at 110° C. for at least 48 hours in vacuo.

Example 5 Preparation of Crosslinked PPO-PEO-PPO-CA-Si Organic-Inorganic Hybrid Polymer Membranes

A catalytic amount of acetic acid 0.01 g, 0.17 mmol) was added to 18.38 g of a polymer solution in 1,4-dioxane or THF containing 0.708 g (2.13 mmol) of crosslinkable CA-organotriethoxysilane prepared in Example 1 and 0.212 g (0.085 mmol) of PPO-PEO-PPO-organotriethoxysilane polymer prepared in Example 3 followed by the addition of 0.01 g, 0.17 mmol) of ethanol. The resulting solution was mixed for at least 6 hours at room temperature. The solution was then filtered through a 0.2 μm PTFE membrane filter. 16.0 g of the filtrate solution containing about 0.8 g of total polymers was cast onto the surface of a clean glass plate, and dried at room temperature for 24 hours. The resulting crosslinked PPO-PEO-PPO-CA-Si hybrid polymer membrane was detached from the glass plate and further dried at 110° C. for at least 48 hours in vacuo. 

1. A process for separating at least one gas from a mixture of gases, the process comprising: a) providing a crosslinked organic-inorganic hybrid polymer membrane comprising a crosslinked organic-inorganic hybrid polymer made from at least two different precursor organic polymers having hydroxyl, amino, epoxy, isocyanato, or dianhydride groups wherein said precursor organic polymers are is selected from the group consisting of poly(ethylene oxide) (PEO), cellulose acetate (CA), poly(propylene oxide) (PPO), co-block-poly(ethylene oxide)-poly(propylene oxide) (PEO-PPO), tri-block-poly(propylene oxide)-poly(ethylene oxide)-poly(propylene oxide) (PPO-PEO-PPO), poly(propylene glycol)-block-poly(ethylene glycol)-block-poly(propylene glycol) bis(2-aminepropyl ether) (PAPE), dendritic PEO, and hyperbranched amine-terminated PEO, and crosslinked with an organosilicon alkoxide crosslinking agent; and b) contacting the mixture of gases to a first side of the crosslinked organic-inorganic hybrid polymer membrane to cause said at least one gas to permeate the mixed matrix membrane; and c) removing from a second side of the membrane a permeate gas composition comprising at least a portion of said at least one gas which permeated said membrane.
 2. The process of claim 1 wherein one of said precursor organic polymers is cellulose acetate.
 3. The process of claim 1 wherein said organosilicon alkoxide crosslinking agent comprises

wherein n=−2-10; m=3; R′ is an organic functional group selected from the group consisting of —(CH₂)_(a)NH₂, —(CH₂)OH, —(CH₂)_(a)NH(CH₂)₂NH₂, OCH₂CH(OH)CH₂N(CH₂CH₂OH)₂, —(CH₂)_(a)N═C═O, —(CH₂)_(a)CH(O)CH₂, and mixtures thereof wherein a=1-20; and wherein R″ is a C₁-C₈ hydrocarbon group.
 4. The process of claim 1 wherein one of said precursor organic polymers is cellulose acetate and at least one of said precursor organic polymers is selected from the group consisting of poly(ethylene oxide) (PEO), poly(propylene oxide) (PPO), co-block-poly(ethylene oxide)-poly(propylene oxide) (PEO-PPO), tri-block-poly(propylene oxide)-poly(ethylene oxide)-poly(propylene oxide) (PPO-PEO-PPO), poly(propylene glycol)-block-poly(ethylene glycol)-block-poly(propylene glycol) bis(2-aminopropyl ether) (PAPE), dendritic PEO, and hyperbranched amine-terminated PEO.
 5. The process of claim 4 wherein one of said precursor organic polymers is cellulose acetate and at least two of said precursor organic polymers are selected from the group consisting of poly(ethylene oxide) (PEO), poly(propylene oxide) (PPO), co-block-poly(ethylene oxide)-poly(propylene oxide)s (PEO-PPO), tri-block-poly(propylene oxide)-poly(ethylene oxide)-poly(propylene oxide) (PPO-PEO-PPO), poly(propylene glycol)-block-poly(ethylene glycol)-block-poly(propylene glycol) bis(2-aminepropyl ether) (PAPE), dendritic PEO, and hyperbranched amine-terminated PEO.
 6. The process of claim 1 wherein one of said precursor organic polymers is cellulose acetate and one of said precursor organic polymers is poly(ethylene oxide).
 7. The process of claim 1 wherein said crosslinked organic-inorganic hybrid polymer membrane comprises a crosslinked poly(ethylene oxide)-cellulose acetate-silsesquioxane organic-inorganic hybrid polymer.
 8. The process of claim 1 wherein said mixture of gases is selected from the group consisting of carbon dioxide and nitrogen; olefins and paraffins; carbon dioxide and methane; aromatics and non-aromatics; water and methane; sulfur dioxide and nitrogen, hydrogen sulfide and methane; ammonia and methane; hydrogen sulfide and nitrogen; hydrogen sulfide and hydrogen, oxygenates and hydrocarbon, nitrogenates and hydrocarbon, and sulfur compounds and hydrocarbon.
 9. The process of claim 1 wherein said mixture of gases is selected from the group consisting of carbon dioxide/methane, carbon dioxide/nitrogen, olefin/paraffin, aromatics/non-aromatics, water, hydrogen sulfide, sulfur dioxide, and ammonia mixtures with methane, nitrogen, hydrogen and air.
 10. The process of claim 9 wherein said mixtures of gases comprises carbon dioxide and nitrogen.
 11. The process of claim 9 wherein said mixtures of gases comprises carbon dioxide and methane. 